CN201454430U - Novel air agitation foaming device - Google Patents

Novel air agitation foaming device Download PDF

Info

Publication number
CN201454430U
CN201454430U CN2009200969556U CN200920096955U CN201454430U CN 201454430 U CN201454430 U CN 201454430U CN 2009200969556 U CN2009200969556 U CN 2009200969556U CN 200920096955 U CN200920096955 U CN 200920096955U CN 201454430 U CN201454430 U CN 201454430U
Authority
CN
China
Prior art keywords
pipeline
outlet
mixing apparatus
metering device
aerated stirring
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Expired - Fee Related
Application number
CN2009200969556U
Other languages
Chinese (zh)
Inventor
刘建华
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Individual
Original Assignee
Individual
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Individual filed Critical Individual
Priority to CN2009200969556U priority Critical patent/CN201454430U/en
Application granted granted Critical
Publication of CN201454430U publication Critical patent/CN201454430U/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

Links

Images

Abstract

The utility model relates to a novel air agitation foaming device consisting of an air intake device, a feeding device and an agitator, wherein the air intake device consisting of an air transmission pipeline, a pressure regulating filtering device and a voltage regulating and current stabilizing metering device. One end of the air transmission pipeline is connected to compressed air, and the air transmission pipeline is provided with the pressure regulating filtering device, the outlet of pressure regulating filtering device is connected with the voltage regulating and current stabilizing metering device. The outlet of the voltage regulating and current stabilizing metering device is connected with the air inlet of a premixing device through a check valve; the discharge hole of the feeding device is connected with the slurry inlet of the premixing device, and the mixture outlet of the premixing device is connected with the feed inlet of the agitating device. The agitating device is a pipeline type high-shearing mixing emulsification device. The utility model has the advantages of scientific and reasonable structure design, accurate control of foaming volume ratio of slurry, even and exquisite foaming effect, easy manufacturing, low cost, low energy consumption, high degree of automation, simple operation, stable running, long service life and the like.

Description

Aerated stirring foam device
Technical field
The utility model belongs to the foam device field, particularly a kind of aerated stirring foam device.
Background technology
At present, in all conglomeraties, all need use foam device.For example, in food industry, in the production of bread, cake, dessert, biscuit, dairy produce, candy, usually need to adopt foam device, to increase the soft crunchy sensation of food with the processing of foaming of some raw material; In leather is produced, in the technology that leather surface is covered with paint, lacquer, colour wash, etc., also coating need be foamed usually, carry out foamed and sprayed or roller coat, hide the leather surface permanent disability, to improve surface quality, improve leather hand feeling, conservation reduces cost simultaneously; At packaging industry and timber multi-layer sheet production field, often adopt the water-based glue, multilayer material is carried out compound, as adopting foam device, not only can save glue, saving oven dry expense that can also be a large amount of; In Non-Woven Fabric Industry, need carry out the back arrangement to the material of producing, adopt foam device can save finishing agent and oven dry expense equally, and make non-weaving cloth obtain better feel and specific function; In dry method paper industry, adopt the glue of foaming that the processing of reduction dust is done on its surface, can make dry method paper obtain the effect of dried fastness to wet rubbing and fluffy softness, obtain considerable economic.
Existing foam device adopts the cylinder agitating device of built-in impeller mostly, and it can only realize mixed function.Also there is the feed entrance point on agitating device to feed compressed air, to reach the purpose that stirs simultaneously and foam.But it is relatively poor that above-mentioned foam device exists compressed air and slurry to mix degree, and problem such as the foaming ratio is wayward influences product quality.And this kind foam device such as need obtain more fine and smooth foaming effect, then must improve motor speed, the agitating device impeller is rotated at a high speed, thereby the portion of carrying out increase the load of foam device motor, and power consumption is high.Also there are many defectives such as manufacture difficulty is big, cost is high, easily break down, service life is short in addition.
Summary of the invention
The purpose of this utility model is to overcome the deficiencies in the prior art, a kind of reasonable in design is provided, is easy to accurately control the aerated stirring foam device of foaming ratio, uniform in foaming exquisiteness.
The utility model solves its technical problem and is achieved through the following technical solutions:
A kind of aerated stirring foam device, constitute by inlet duct, feed arrangement and agitating device, it is characterized in that: described inlet duct is made of gas transfer pipeline, pressure regulation filter, voltage stabilization and current stabilization metering device, one end of gas transfer pipeline connects compressed air, the pressure regulation filter is installed on the gas transfer pipeline, the outlet of pressure regulation filter connects the voltage stabilization and current stabilization metering device, and the outlet of voltage stabilization and current stabilization metering device connects the gas feed of a pre-mixing apparatus by a non-return valve; The discharging opening of described feed arrangement is connected with the slurry import of pre-mixing apparatus, and the compound outlet of pre-mixing apparatus is connected with the charging aperture of agitating device, and this agitating device is a pipeline high shear mixing emulsifier unit.
And described feed arrangement is a single-screw (single screw) pump, and the drive motors of this single-screw (single screw) pump is connected with a frequency converter.
And, gas transfer pipeline between pressure regulation filter and the voltage stabilization and current stabilization metering device is provided with pressure sensor, gas transfer pipeline between voltage stabilization and current stabilization metering device and the pre-mixing apparatus is provided with another pressure sensor, this two pressure sensor all is connected with the signal input part of a controller, and the signal output part of this controller is connected with the voltage stabilization and current stabilization metering device.
And described frequency converter is connected with controller.
And the stratiform stainless steel porous plate filler that described pre-mixing apparatus is radially installed by tubular shell and inner institute constitutes, and is shaped on gas feed and slurry import at an end of tubular shell, is shaped on compound at the other end of tubular shell and exports.
And, between single-screw (single screw) pump and pre-mixing apparatus, be connected the clean water pipeline by valve.
And, be connected and installed the pulp pipeline at the grout outlet of high shear mixing emulsifier unit, a magnetic valve is installed on the pulp pipeline, this magnetic valve is controlled by a time relay.
And, in the end of pulp pipeline the sizing head being installed, this sizing head is installed on the slide, and this slide is movably installed on the guide rail, and slide is moved back and forth along guide rail by drive mechanism.
And, two sizing heads are installed on described pulp pipeline, this two sizings head symmetry is installed on separately on the slide, and its slide is movably installed in respectively on the guide rail, and two slides all move back and forth along guide rail separately synchronously by drive mechanism.
Advantage of the present utility model and beneficial effect are:
1. this aerated stirring foam device adopts pipeline high shear mixing emulsifier unit that mixed slurry is carried out the high speed shear stirring, can effectively improve the foaming effect of slurry, the foaming that makes slurry is uniform and smooth more, and energy consumption is low, stable, long service life.
2. the control of passing through voltage stabilization and current stabilization metering device and frequency converter of this aerated stirring foam device can realize the accurate control to admission pressure and inlet amount, thereby the control foam volume is than accurate more, stable.
3. the compressed air and the slurry of this aerated stirring foam device enter pre-mixing apparatus jointly, and in pre-mixing apparatus, fully mix under the effect of set stratiform stainless steel porous plate filler, more existing jet blower more can make liquid fully mix with gas reliably, also can guarantee the continous-stable discharging simultaneously.
4. be connected the clean water pipeline by valve between the single-screw (single screw) pump of this aerated stirring foam device and the pre-mixing apparatus; after foaming is finished and is shut down; adopt purging system that single-screw (single screw) pump, pre-mixing apparatus and pipeline high shear mixing emulsifier unit are cleaned; remain in device inside with slurry-free, influence operate as normal.
5. the pulp pipeline installed of this aerated stirring foam device high shear mixing emulsifier unit is provided with magnetic valve, and by the unlatching and the shut-in time of time relay control magnetic valve, its purpose is to control the time of slurry in high shear mixing emulsifier unit internal stops, makes slurry fine and smooth more, even.
6. this aerated stirring foam device is equipped with the sizing head on the pulp pipeline that the high shear mixing emulsifier unit is installed, the sizing head is moved back and forth along guide rail by drive mechanism, because the flowability of the slurry after this inflating and stirring device of process is handled reduces, therefore, sizing head by the activity setting can be coated slurry the whole breadth of pending product more uniformly, and, can adopt the mode that is symmetrical arranged the sizing head to carry out synchronous pasting and handle as needing double spread.
7. the utility model scientific structure design is reasonable, can accurately control the foam volume ratio of slurry, the foaming effect uniform and smooth, have simultaneously be easy to manufacture, advantages such as cost is low, energy consumption is little, automaticity is high, simple to operate, stable, long service life.
Description of drawings
Fig. 1 is an operation principle schematic diagram of the present utility model;
Fig. 2 is the structural representation (partly cuing open figure) of pre-mixing apparatus of the present utility model;
Fig. 3 is the structural representation (being installed on the roller coating device top) of the utility model sizing head;
Fig. 4 is the vertical view of Fig. 3.
The specific embodiment
The utility model is described in further detail below by specific embodiment, and following examples are descriptive, is not determinate, can not limit protection domain of the present utility model with this.
A kind of aerated stirring foam device is made of inlet duct, feed arrangement and agitating device, and its innovation part is: inlet duct is made of gas transfer pipeline, pressure regulation filter, voltage stabilization and current stabilization metering device.One end of gas transfer pipeline connects compressed air, the pressure regulation filter is installed on the gas transfer pipeline, the outlet of pressure regulation filter connects the voltage stabilization and current stabilization metering device, make the air pressure of being measured more accurate, course of conveying is more stable, be not subjected to the influence of pipeline compressed air pressure in early stage, the outlet of voltage stabilization and current stabilization metering device connects the gas feed of pre-mixing apparatus by a non-return valve.
Feed arrangement is a single-screw (single screw) pump, and the drive motors of this single-screw (single screw) pump is connected with a frequency converter, and the discharging opening of single-screw (single screw) pump is connected with the slurry import of pre-mixing apparatus.
As shown in Figure 2, pre-mixing apparatus is made of tubular shell 2 and the inner stratiform stainless steel porous plate filler of being installed 3, end at tubular shell is shaped on gas feed 4 and slurry import 5, be shaped on the outlet 1 of compound at the other end of tubular shell, the compound outlet is connected with the charging aperture of agitating device, and this agitating device is a pipeline high shear mixing emulsifier unit.Be connected the clean water pipeline by valve between single-screw (single screw) pump and pre-mixing apparatus, the water inlet of clean water pipeline feeds cleaning water.
The stirring-head of pipeline high shear mixing emulsifier unit is formed by a plurality of separate chamber polyphones that are made of rotor stator, gas-liquid mixture moves to the process of another chamber from a chamber, obtain sufficient shear action, make two phase flow fully be mixed into a phase, realize the refinement of gas-liquid mixture, make the foam of the foaming slurry that is obtained evenly fine and smooth more.Because stirring-head can be organized polyphone more and use, so it has the advantage that cost is low, reliability is good, in addition, owing to adopt associated mode between each stirring-head and the drive motors, does not need its speed is regulated, make and operation more simple and easy to do.At pipeline high shear mixing emulsifier unit outer setting cooling system, this cooling system can be for being arranged on the water jacket of emulsifier unit outside, and water jacket is connected with cooling water pipeline, and the water inlet of cooling water pipeline feeds cooling water.Thereby can reduce the operating temperature of device, the job stability of holdout device integral body.
Gas transfer pipeline between pressure regulation filter and the voltage stabilization and current stabilization metering device is provided with pressure sensor, pipeline between voltage stabilization and current stabilization metering device and the pre-mixing apparatus is provided with another pressure sensor, the signal input part of this two pressure sensors homogeneous controller connects, and the signal output part of this controller is connected with the voltage stabilization and current stabilization metering device.The signal output part of this controller also links to each other with frequency converter.By control, can make more accurate, the more stable metering of desired compression air acquisition in the course of work to the voltage stabilization and current stabilization metering device; Regulate the single-screw (single screw) pump rotating speed by frequency converter, realizing metering and pressure control to slurry, thereby the control foam volume than more accurately, stable.Have the automaticity height, simple to operate, the advantage that is easy to control.
Grout outlet at the high shear mixing emulsifier unit is connected and installed the pulp pipeline, and a magnetic valve is installed on the pulp pipeline, and this magnetic valve is controlled by a time relay.By the unlatching and the shut-in time of time relay control magnetic valve, its purpose is to prolong the time of slurry in high shear mixing emulsifier unit internal stops, makes slurry fine and smooth more, even.
Sizing 6 also can be installed in the end of pulp pipeline 8, this sizing head is installed on the slide 7, this slide is movably installed on the guide rail 12, slide is moved back and forth along guide rail by drive mechanism. and above-mentioned guide rail and driving mechanism all are installed on the top of roller coating device by frame. in the present embodiment, two sizing heads are installed on the pulp pipeline, this two sizings head symmetry is installed on separately on the slide, its slide is movably installed in respectively on separately the guide rail, two slides all move back and forth along guide rail separately synchronously by drive mechanism. and driving mechanism adopts the sprocket wheel chain drive mechanism, the sprocket chain strip transmission mechanism that two slides are installed is for being symmetrical arranged, link by power transmission shaft 11 between its symmetrical sprocket wheel 13, the coaxial drive sprocket 10 that installs on the power transmission shaft therein, this drive sprocket is installed by drive sprocket (not label) interlock that chain and stepper motor 9 output shafts are installed. and drive by stepper motor and realize moving back and forth synchronously of two slides. at slide block original position institute installation position displacement sensor 14, and by the stroke of controller by the step motor control slide block. and, by controller the slide block translational speed is set. by moving back and forth of sizing head, can make slurry coat the whole breadth of product more uniformly.
Operation principle of the present utility model is:
Compressed air at first enters the pressure regulation filter, obtain to enter the voltage stabilization and current stabilization metering device behind the system works pressure, compressed air is accurately entering pre-mixing apparatus inside behind control flow and the pressure, through pre-mixing apparatus compressed air and slurry are fully mixed, enter high shear mixing emulsifier unit inside then and carry out high-speed stirred, thus finish the foaming slurry the foam thinning process.The foaming slurry is evenly coated product surface by the sizing head of activity setting.After foaming is finished and shut down, adopt purging system that single-screw (single screw) pump, pre-mixing apparatus and pipeline high shear mixing emulsifier unit are cleaned.

Claims (9)

1. aerated stirring foam device, constitute by inlet duct, feed arrangement and agitating device, it is characterized in that: described inlet duct is made of gas transfer pipeline, pressure regulation filter, voltage stabilization and current stabilization metering device, one end of gas transfer pipeline connects compressed air, the pressure regulation filter is installed on the gas transfer pipeline, the outlet of pressure regulation filter connects the voltage stabilization and current stabilization metering device, and the outlet of voltage stabilization and current stabilization metering device connects the gas feed of a pre-mixing apparatus by a non-return valve; The discharging opening of described feed arrangement is connected with the slurry import of pre-mixing apparatus, and the compound outlet of pre-mixing apparatus is connected with the charging aperture of agitating device, and this agitating device is a pipeline high shear mixing emulsifier unit.
2. aerated stirring foam device according to claim 1 is characterized in that: described feed arrangement is a single-screw (single screw) pump, and the drive motors of this single-screw (single screw) pump is connected with a frequency converter.
3. aerated stirring foam device according to claim 1, it is characterized in that: the gas transfer pipeline between pressure regulation filter and the voltage stabilization and current stabilization metering device is provided with pressure sensor, gas transfer pipeline between voltage stabilization and current stabilization metering device and the pre-mixing apparatus is provided with another pressure sensor, this two pressure sensor all is connected with the signal input part of a controller, and the signal output part of this controller is connected with the voltage stabilization and current stabilization metering device.
4. aerated stirring foam device according to claim 2, it is characterized in that: described frequency converter is connected with controller.
5. according to claim 1 or 3 described aerated stirring foam devices, it is characterized in that: described pre-mixing apparatus by tubular shell and inner institute radially the stratiform stainless steel porous plate filler of installation constitute, end at tubular shell is shaped on gas feed and slurry import, is shaped on the compound outlet at the other end of tubular shell.
6. aerated stirring foam device according to claim 2 is characterized in that: be connected the clean water pipeline by valve between single-screw (single screw) pump and pre-mixing apparatus.
7. aerated stirring foam device according to claim 1 is characterized in that: the grout outlet at the high shear mixing emulsifier unit is connected and installed the pulp pipeline, and a magnetic valve is installed on the pulp pipeline, and this magnetic valve is controlled by a time relay.
8. aerated stirring foam device according to claim 7, it is characterized in that: the sizing head is installed in the end of pulp pipeline, this sizing head is installed on the slide, and this slide is movably installed on the guide rail, and slide is moved back and forth along guide rail by drive mechanism.
9. aerated stirring foam device according to claim 7, it is characterized in that: two sizing heads are installed on described pulp pipeline, this two sizings head symmetry is installed on separately on the slide, its slide is movably installed in respectively on the guide rail, and two slides all move back and forth along guide rail separately synchronously by drive mechanism.
CN2009200969556U 2009-06-02 2009-06-02 Novel air agitation foaming device Expired - Fee Related CN201454430U (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN2009200969556U CN201454430U (en) 2009-06-02 2009-06-02 Novel air agitation foaming device

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN2009200969556U CN201454430U (en) 2009-06-02 2009-06-02 Novel air agitation foaming device

Publications (1)

Publication Number Publication Date
CN201454430U true CN201454430U (en) 2010-05-12

Family

ID=42381775

Family Applications (1)

Application Number Title Priority Date Filing Date
CN2009200969556U Expired - Fee Related CN201454430U (en) 2009-06-02 2009-06-02 Novel air agitation foaming device

Country Status (1)

Country Link
CN (1) CN201454430U (en)

Cited By (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN102318653A (en) * 2011-06-01 2012-01-18 吴仲彬 Automatic cake foam maker
CN104069765A (en) * 2014-06-27 2014-10-01 浙江圣诺盟顾家海绵有限公司 Full-automatic foaming machine
CN107415126A (en) * 2017-05-19 2017-12-01 嘉善双杰海绵有限公司 A kind of continous way sponge foaming device
CN108497954A (en) * 2018-04-16 2018-09-07 安捷睿(厦门)机器人有限公司 A kind of parametrization dismisses system and liquid transporting apparatus and air transporting arrangement in real time
CN109130055A (en) * 2018-08-30 2019-01-04 苏州科易特自动化科技有限公司 A kind of full-automatic emulsion foaming machine and its control system
CN109748353A (en) * 2019-02-22 2019-05-14 东北师范大学 The device and method for treating water of water process are carried out based on flow control microvesicle-ozone coupling
CN110353071A (en) * 2019-08-22 2019-10-22 湖南元晟食品贸易有限公司 Pre-mixing apparatus and inflator

Cited By (9)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN102318653A (en) * 2011-06-01 2012-01-18 吴仲彬 Automatic cake foam maker
CN102318653B (en) * 2011-06-01 2014-01-08 吴仲彬 Automatic cake foam maker
CN104069765A (en) * 2014-06-27 2014-10-01 浙江圣诺盟顾家海绵有限公司 Full-automatic foaming machine
CN104069765B (en) * 2014-06-27 2016-02-24 浙江圣诺盟顾家海绵有限公司 Full-automatic foaming machine
CN107415126A (en) * 2017-05-19 2017-12-01 嘉善双杰海绵有限公司 A kind of continous way sponge foaming device
CN108497954A (en) * 2018-04-16 2018-09-07 安捷睿(厦门)机器人有限公司 A kind of parametrization dismisses system and liquid transporting apparatus and air transporting arrangement in real time
CN109130055A (en) * 2018-08-30 2019-01-04 苏州科易特自动化科技有限公司 A kind of full-automatic emulsion foaming machine and its control system
CN109748353A (en) * 2019-02-22 2019-05-14 东北师范大学 The device and method for treating water of water process are carried out based on flow control microvesicle-ozone coupling
CN110353071A (en) * 2019-08-22 2019-10-22 湖南元晟食品贸易有限公司 Pre-mixing apparatus and inflator

Similar Documents

Publication Publication Date Title
CN201454430U (en) Novel air agitation foaming device
CN111432955A (en) Integrated sand mixer and sand mixing method
CN111152378A (en) Mixing device for producing rubber and plastic heat-insulating material
CN216224123U (en) Cement air stirrer
CN215311806U (en) Paper pulp slurry mixing device
CN214020163U (en) Solid-liquid mixing device
CN112852536A (en) A compounding mixer for production of sesame oil
CN211659859U (en) Compound circulating device of pumping agent
CN209576356U (en) A kind of environment-friendlyink ink material mixer
CN102275640B (en) Static mixing type filling machine
CN107596974A (en) A kind of intelligent coating material agitator
KR101153849B1 (en) Koji making machine
CN208035055U (en) A kind of kneading device for producing high evenness tire
CN214353736U (en) Latex foam maker for producing latex pillow with uniform mixing
CN217196279U (en) A high-speed mixer for production of antistatic fire-retardant PVC board
CN206199263U (en) A kind of reaction unit for producing aqueous adhesive
CN204487801U (en) Slip casting system
CN209771886U (en) Milk barrel lid production is with even machine of mixing colours of colour mixture
CN208694771U (en) A kind of chemical industry mixing tank of good damping effect
CN219445435U (en) Feeding mechanism for roller of density board
CN202115714U (en) Static mixing type filling machine
CN201316701Y (en) Paint flow control device
CN221753108U (en) Raw material mixing device
CN214394736U (en) Full-automatic mixer is used in diatom mud coating production
CN218700042U (en) Gypsum foaming machine is used in production of environmental protection whitewash gypsum

Legal Events

Date Code Title Description
C14 Grant of patent or utility model
GR01 Patent grant
C17 Cessation of patent right
CF01 Termination of patent right due to non-payment of annual fee

Granted publication date: 20100512

Termination date: 20110602